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TW201119738A - Method for manufacturing large-diameter titanium-silicon molecular sieve and method for manufacturing cyclohexanone oxime using such a molecular sieve - Google Patents

Method for manufacturing large-diameter titanium-silicon molecular sieve and method for manufacturing cyclohexanone oxime using such a molecular sieve Download PDF

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TW201119738A
TW201119738A TW098142427A TW98142427A TW201119738A TW 201119738 A TW201119738 A TW 201119738A TW 098142427 A TW098142427 A TW 098142427A TW 98142427 A TW98142427 A TW 98142427A TW 201119738 A TW201119738 A TW 201119738A
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titanium
molecular sieve
flocculant
hour
range
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TW098142427A
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TWI399242B (en
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Pin-To Yao
Cheng-Fa Hsieh
Shih-Yao Chao
Yang-Min Liang
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China Petrochemical Dev Corp Taipei Taiwan
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Priority to TW098142427A priority Critical patent/TWI399242B/en
Priority to US12/748,932 priority patent/US8540956B2/en
Priority to JP2010274894A priority patent/JP5437984B2/en
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J29/00Catalysts comprising molecular sieves
    • B01J29/04Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites
    • B01J29/06Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
    • B01J29/40Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of the pentasil type, e.g. types ZSM-5, ZSM-8 or ZSM-11, as exemplified by patent documents US3702886, GB1334243 and US3709979, respectively
    • B01J29/405Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of the pentasil type, e.g. types ZSM-5, ZSM-8 or ZSM-11, as exemplified by patent documents US3702886, GB1334243 and US3709979, respectively containing rare earth elements, titanium, zirconium, hafnium, zinc, cadmium, mercury, gallium, indium, thallium, tin or lead
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B37/00Compounds having molecular sieve properties but not having base-exchange properties
    • C01B37/005Silicates, i.e. so-called metallosilicalites or metallozeosilites
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B39/00Compounds having molecular sieve and base-exchange properties, e.g. crystalline zeolites; Their preparation; After-treatment, e.g. ion-exchange or dealumination
    • C01B39/02Crystalline aluminosilicate zeolites; Isomorphous compounds thereof; Direct preparation thereof; Preparation thereof starting from a reaction mixture containing a crystalline zeolite of another type, or from preformed reactants; After-treatment thereof
    • C01B39/023Preparation of physical mixtures or intergrowth products of zeolites chosen from group C01B39/04 or two or more of groups C01B39/14 - C01B39/48
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B39/00Compounds having molecular sieve and base-exchange properties, e.g. crystalline zeolites; Their preparation; After-treatment, e.g. ion-exchange or dealumination
    • C01B39/02Crystalline aluminosilicate zeolites; Isomorphous compounds thereof; Direct preparation thereof; Preparation thereof starting from a reaction mixture containing a crystalline zeolite of another type, or from preformed reactants; After-treatment thereof
    • C01B39/04Crystalline aluminosilicate zeolites; Isomorphous compounds thereof; Direct preparation thereof; Preparation thereof starting from a reaction mixture containing a crystalline zeolite of another type, or from preformed reactants; After-treatment thereof using at least one organic template directing agent, e.g. an ionic quaternary ammonium compound or an aminated compound

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • General Life Sciences & Earth Sciences (AREA)
  • Geology (AREA)
  • Materials Engineering (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Inorganic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • Catalysts (AREA)
  • Silicates, Zeolites, And Molecular Sieves (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)

Abstract

A method for manufacturing large-diameter titanium-silicon molecular sieve comprises preparing first grade crystalline particle molecular sieve dispersion liquid; adding flocculant and coagulant aid to the dispersion liquid to flocculate the particles and form a particle-flocculated solution; mixing the particle-flocculated solution with synthetic rubber of titanium-silicon template; and performing a hydrothermal step. The titanium-silicon molecular sieve manufactured with this method has an average particle diameter greater than 5 micrometer and can be used as a catalyst, whereby when used in manufacturing cyclohexanone oxime, it provides high conversion rate and selection rate and also features the advantage of easy filtration for recycling.

Description

201119738 , 六、發明說明:201119738, VI, invention description:

I 【發明所屬之技術領域】 本發明係有關一種鈦-矽分子篩之製法,特言之,係 關於一種之大粒徑鈦-矽分子筛之製法。 【先前技術】 結晶鈦-矽分子篩係將鈦原子引入二氧化矽的網狀結 構中,具有MFI構造的晶形,亦稱TS-1分子篩。而此分 子篩被大量應用於以雙氧水為氧化劑的氧化反應中作為觸 鲁媒,其製法已揭露於美國第4410501號發明專利。但此方 法所產出之分子篩顆粒大約為0.2微米。然而,0.2微米之 觸媒於化工製程應用中(如利用環己酮、氨及雙氧水等反 應物以鈦矽分子篩為觸媒製備環己酮肟之應用中)面臨極 大挑戰。因此,後續之發明者均致力於發展加大粒徑分子 篩的技術。美國第5500199號、第6106803號及第6524984 號專利教示以無機黏著劑將小顆粒觸媒聚集後經喷霧乾燥 φ 造粒,此方法雖可將觸媒顆粒變大,但具有因觸媒活性基 被黏著劑掩蓋及活性基被稀釋所造成之反應活性不足及必 需增加觸媒用量,俾維持相同之催化功效之缺點。 因此,如何克服上述缺點實已為迫切待解之課題。產 業上仍需要一種可製備具有大粒徑及高活性之鈦-矽分子 篩之方法,其可克服傳統回收分子篩之困難、提昇雙氧水 使用效率及適用於產業上之應用。 【發明内容】 鑒於以上所述習知技術之缺失,本發明即提供一種大 3 11132] 201119738 ( ^經鈦-石夕分子_之製法,包括··準備第—級結晶顆粒分子 師白It散液;於上述分散液中加入絮凝劑及助凝劑,使顆 粒♦本,形成聚集顆粒溶液;混合該聚集顆粒溶液與鈦_ 矽模板劑合成膠;以及進行水熱步驟。本發明製法所形成 之鈦-石夕分子_具有5微米以上之平均粒徑,作為製. 嗣肪之觸媒時,不但可達到高轉化率與選擇率,更兼呈有 易於過濾分離之優點。 八有 【實施方式】 以下係藉由特定的具體實例說明本創作之實施方 ί解技Γ人士可由本說明書所揭示之内容輕易地 ,、、— 之優點及功效。本創作亦可以其它不同的方式 予以貝施’即’在不‘_本創作所揭示之技術思想之前提 下,能予不同之修飾與改變。 本發明之製法係使用已完成水熱之未_分子筛粉 末(TS]、S-U其組合)作為第一級結晶顆粒之分子筛,將 =弟-^結晶顆粒分子筛粉末分散於水中形成分散液然 後加入I賴及助凝劑使顆粒聚集,形成聚集顆粒之水溶 液’再^合具有該聚集顆粒之水溶液以及鈦板劑合成 膝’取後將此混合物密封於鐵氟龍内襯不鏽鋼耐壓罐中進 订水熱步驟。种H級結晶難之分子篩與該欽· 矽杈板劑合成膠混合之重量比範圍係介於广⑺至綱, 較佳係介於1:]G至1 :咖,更佳係介於】:H)至]:谓, 又更佳係介於1 : 11.6至i : 167。 本發明製法所使用的絮凝劑為高分子絮凝劑。更具體 1Π321 4 201119738 而言,本發明之絮凝劑種類可遂自於陽離子絮凝劑、陰離 子絮凝劑、兩性絮凝劑或其組舍。該陽離子絮凝劑的實例 包括季銨鹽聚合物(諸如:二甲基-二烯丙基氯化銨聚合物 或聚甲基丙烯酸三甲铵基乙酯聚合物)、聚乙敍或聚乙烯0比 °定,或其組合;陰離子絮凝劍的貫例包括聚丙稀酸納與丙 烯醯銨共聚物、丙烯酸鈉與丙烯醯銨共聚物或其組合;兩 性絮凝劑的實例包括丙烯酸季鉉朦與丙烯酸鈉的共聚物。 一般而言,本發明製法所使用之兩分子絮凝劑之平均分子 量至少為100,000以上,較佳為100,000至2〇,麵,〇〇〇。該 絮凝劑可以水溶液的方式添加。通常’該絮凝劑水溶液之 濃度(重量百分比)範圍為0,1炱1重量% ’較佳為0.2至 0.8重量%,又更佳為〇.3至0.6重量%之範圍。該絮凝劑 用量,以100克之鈦-矽模板劑合成膠計’係使用0.0001 至〇.05克,較佳係使用0.0001 1 0.03克’更佳係使用0.001 至0.025克。 本發明所使用的助凝劑可為矽酸醋、聚乙氧基矽烷或 —氧化矽膠體溶液。該矽酸酯的實例包括四曱基矽酸酷、 四己基矽酸酯、四丙基矽酸酯、四丁基矽酸酯或其組合; 该聚乙氧基矽烷可的實例包括ES-28(n=l至2)、ES-32(n=3 至4)、ES-40(n=4至5)或其組合;以及該二氧化矽膠體溶 液的實例包括購自杜邦公司之Ludox AS-40、Ludox 、Ludox AM-30、Ludox TM-40、Ludox TM-50、Ludox A^[~3〇、Ludox HS-30、Ludox HS-40 或其組合。本發明之 製法中,該助凝劑之使用量,以100克之鈦-矽模板劑合成 201119738 f〇f 係使用o.1至6克之助凝劑,較佳係使用0.1至3 克之助凝劑。 於-具體實例中,本發明製法所使用之鈦·㈣板劑 合成膠係藉由下述方法製備:首先,先將鈦源(例如,四烷 f欽㈣、三氯化鈦、吨化鈦、及硫酸鈦等)置於反應容 〇口遲該具體貫例中,係將該鈦源置於氮封單頸瓶中。接 著將系統溫度降至穴,將溶劑(例如,無水異丙醇或水) 庄入上述II封單頸瓶中,_ 15分鐘。接著,利用等壓加 ,漏:將矽源(例如,四烷基矽酸酯、矽膠、矽溶膠)滴入 氮封單頸瓶中,滴加完成後持續進行授拌,歷時!小時。 丄見拌7U成後利用荨塵加料漏斗將模板劑(例如,四丙基 氫氧化銨)滴人氮封單頸瓶中,滴加完成後再持續進行ς ^歷時1小時。最後,待系統溫度回溫至常溫後,去除 浴劑,即得到鈦_矽模板劑合成膠(例如,在肋。c之條件下 進形除醇,歷時2小時)。-般而言,本發明製造該欽涪 模板劑合成膠之反應製程中,所使用之鈦源和矽源之莫耳 比範圍為0.005 : 1至0.06 : 1,較佳為〇 〇15 : j至〇 〇5 . 更佳為0.02 : i至0.045 : !。所使用之模板劑和石夕源之 莫耳比範圍為0.1 : i至〇·5 :丨,較佳為〇 15 : 1至Μ · 卜*更佳為0·2: 1 m 1。所使用之無水異㊉醇和石夕源 之莫耳比範圍為1 : 1至4.5 : 1,較佳為18 : i至3 5 . /、 更佳為2.2:1至3:卜所使用之水和石夕源之莫耳比為10. j至80 : 1,較佳為2〇 :丨至6〇 :丨,更佳為邓:1至. 111321 6 201119738 本發明之製法巾,該水熱步料湘水作為介質,外 加適當的溫度,在密閉的反應器内產生壓力,進行反應。 於-舉體實例中,本發明係藉由水熱法,利用鐵氣龍内概 不鏽鋼耐壓罐作為反應器,將反應器旋緊、密閉後,放入 加熱爐中進行反應,製作大粒徑鈦-石夕分子筛…般而言, 本發明製法所進行之水熱步驟之溫度係介於1〇叱至22〇 C之間’較佳為15G°C至18G°C。水熱步驟之時間範圍為 馨72小時至24G小時,較佳為12()小時至192小時。 本!X月之衣法亦可在水熱步驟完成後,將固體與液體 分固體部分以水洗至中性,再經供乾及锻燒,獲得用 ;衣己酉轉之大粒;^鈦_石夕分子_觸媒。—般來說,锻燒溫 度於450 C至650°C之間,較佳為5()(rc至5贼,炮 燒時間係介於6小時至則、時之間,較佳為12小時至% 小時。TECHNICAL FIELD OF THE INVENTION The present invention relates to a process for producing a titanium-bismuth molecular sieve, and more particularly to a process for producing a large-diameter titanium-ruthenium molecular sieve. [Prior Art] The crystalline titanium-germanium molecular sieve system introduces titanium atoms into the network structure of cerium oxide, and has a crystal form of an MFI structure, also known as a TS-1 molecular sieve. However, this molecular sieve has been widely used as a ruthenium in an oxidation reaction using hydrogen peroxide as an oxidizing agent, and its preparation method has been disclosed in U.S. Patent No. 4,410,501. However, the molecular sieve particles produced by this method are approximately 0.2 microns. However, 0.2 micron catalysts are extremely challenging in chemical process applications such as the use of cyclohexanone, ammonia, and hydrogen peroxide to produce cyclohexanone oxime using a titanium ruthenium molecular sieve as a catalyst. Therefore, the inventors of the following are all committed to the development of techniques for increasing the size of molecular sieves. U.S. Patent Nos. 5,500,199, 6,106,803 and 6,524,984 teach the polymerization of small particle catalysts by inorganic binders and spray-drying granulation. This method can increase the catalyst particles but has catalytic activity. The base is covered by the adhesive and the reactive group is diluted to have insufficient reactivity and it is necessary to increase the amount of the catalyst to maintain the same catalytic effect. Therefore, how to overcome the above shortcomings has become an urgent issue. There is still a need in the industry for a method for preparing a titanium-germanium molecular sieve having a large particle size and high activity, which overcomes the difficulties of conventional molecular sieve recovery, enhances the efficiency of hydrogen peroxide use, and is suitable for industrial applications. SUMMARY OF THE INVENTION In view of the above-mentioned shortcomings of the prior art, the present invention provides a method for producing a large 3 11132] 201119738 (^ by Titanium-Shixi molecule), including · preparing a first-order crystalline particle molecular master white it a flocculating agent and a coagulant are added to the dispersion to form a granule solution; the aggregated granule solution is mixed with a titanium ruthenium templating agent; and a hydrothermal step is carried out. The method of the present invention is formed. The titanium-Shixi molecule has an average particle diameter of 5 micrometers or more. As a catalyst for the fat, it can not only achieve high conversion rate and selectivity, but also has the advantages of easy filtration and separation. MODES OF THE INVENTION The following is a specific example to illustrate the implementation of the author. The technical person can easily reveal the advantages and functions of the content disclosed in this specification. This creation can also be applied in other different ways. 'Immediately' can be modified and changed before the technical idea disclosed in this creation. The method of the present invention uses the hydrothermal un-molecular sieve powder (TS), SU. a combination thereof) as a molecular sieve of the first-stage crystal particles, dispersing the powder of the molecular sieve molecular sieve in water to form a dispersion, and then adding the I and the coagulant to aggregate the particles to form an aqueous solution of the aggregated particles. The aqueous solution of the aggregated particles and the titanium plate are synthesized and the mixture is sealed in a Teflon-lined stainless steel pressure-resistant tank to prepare a hydrothermal step. The molecular sieve of the H-grade crystal is difficult to synthesize with the Qin·矽杈 plate The weight ratio of the glue mixture is in the range of (7) to the general, preferably between 1:]G to 1: coffee, and more preferably between: H) to::, and more preferably between 1: 11.6 to i: 167. The flocculating agent used in the process of the present invention is a high-molecular flocculant. More specifically, 1 321 4 201119738, the flocculant of the present invention may be derived from a cationic flocculant, an anionic flocculant, an amphoteric flocculant or a combination thereof. Examples of the cationic flocculant include quaternary ammonium salt polymers such as dimethyl-diallyl ammonium chloride polymer or polymethylammonium methacrylate polymer, polyethylene or polyethylene. °, or a combination thereof; examples of anionic flocculation swords include sodium polyacrylate and propylene yttrium ammonium copolymers, sodium acrylate and propylene yttrium ammonium copolymers or combinations thereof; examples of amphoteric flocculants include quaternary acrylic acid and sodium acrylate Copolymer. In general, the two molecules of flocculant used in the process of the present invention have an average molecular weight of at least 100,000 or more, preferably 100,000 to 2 Å, face, 〇〇〇. The flocculant can be added as an aqueous solution. Usually, the concentration (% by weight) of the aqueous flocculant solution is in the range of 0,1炱1% by weight, preferably 0.2 to 0.8% by weight, and more preferably in the range of 0.3 to 0.6% by weight. The flocculating agent is used in an amount of from 0.0001 to 〇.05 g, preferably from 0.0001 1 0.03 g, more preferably from 0.001 to 0.025 g, based on 100 g of the titanium-ruthenium template. The coagulant used in the present invention may be a citric acid vinegar, a polyethoxy decane or a cerium oxide colloidal solution. Examples of the phthalic acid ester include tetradecanoic acid, tetrahexyl phthalate, tetrapropyl phthalate, tetrabutyl phthalate or a combination thereof; examples of the polyethoxy decane include ES-28 (n=l to 2), ES-32 (n=3 to 4), ES-40 (n=4 to 5) or a combination thereof; and examples of the cerium oxide colloidal solution include Ludox AS available from DuPont -40, Ludox, Ludox AM-30, Ludox TM-40, Ludox TM-50, Ludox A^ [~3〇, Ludox HS-30, Ludox HS-40 or a combination thereof. In the preparation method of the present invention, the coagulant is used in an amount of 100 g of a titanium-ruthenium template to synthesize 201119738 f〇f using a coagulant of 0.1 to 6 g, preferably 0.1 to 3 g of a coagulant. . In a specific example, the titanium (4) plate synthetic gel used in the process of the present invention is prepared by the following method: First, a titanium source (for example, tetradecane f (tetra), titanium trichloride, titanium hydride) The titanium source is placed in the nitrogen-sealed single-necked bottle. The system temperature is then lowered to the well and a solvent (eg, anhydrous isopropanol or water) is placed in the above-mentioned II single-necked flask for -15 minutes. Then, using equal pressure addition, leakage: the source of lanthanum (for example, tetraalkyl phthalate, yttrium, cerium sol) is dropped into a nitrogen-sealed single-necked bottle, and the mixing is continued after the completion of the dropwise addition, for a long time! hour. After the mixture was mixed, the templating agent (for example, tetrapropylammonium hydroxide) was dropped into a nitrogen-sealed single-necked flask by a whisker addition funnel, and the hydrazine was continuously continued for 1 hour. Finally, after the temperature of the system is returned to normal temperature, the bath is removed, and a titanium-ruthenium template synthetic rubber is obtained (for example, the alcohol is removed under the condition of rib.c for 2 hours). In general, in the reaction process for producing the enamel templating agent synthetic rubber of the present invention, the molar ratio of the titanium source and the cerium source used is 0.005:1 to 0.06:1, preferably 〇〇15:j. To 〇〇 5. More preferably 0.02 : i to 0.045 : !. The molar ratio of the templating agent used and the shixi source is 0.1: i to 〇·5: 丨, preferably 〇 15 : 1 to Μ · 卜 * more preferably 0·2: 1 m 1 . The molar ratio of anhydrous isodecyl alcohol and Shixiyuan used is from 1:1 to 4.5:1, preferably from 18:i to 3 5 . /, more preferably from 2.2:1 to 3: water used The molar ratio of the stone and the eve of the eve is 10. j to 80: 1, preferably 2 〇: 丨 to 6 〇: 丨, more preferably Deng: 1 to. 111321 6 201119738 The method of the invention, the water heat The step water is used as a medium, and an appropriate temperature is applied to generate pressure in the closed reactor to carry out the reaction. In the example of the invention, the present invention utilizes a hydrothermal method to utilize a stainless steel pressure tank of the iron gas cylinder as a reactor, and the reactor is screwed and sealed, and then placed in a heating furnace for reaction to prepare a large particle. Diameter Titanium-Stone molecular sieve In general, the temperature of the hydrothermal step carried out by the process of the present invention is between 1 Torr and 22 Torr C, preferably 15 G ° C to 18 G ° C. The hydrothermal step has a time ranging from 72 hours to 24 G hours, preferably from 12 () hours to 192 hours. This! X month clothing method can also be completed after the hydrothermal step, the solid and liquid solid parts are washed with water to neutral, and then dried and calcined to obtain; the clothes have been turned into large grains; Shi Xi molecule _ catalyst. In general, the calcination temperature is between 450 C and 650 ° C, preferably 5 () (rc to 5 thieves, the calcination time is between 6 hours and then between hours, preferably 12 hours). To % hours.

,本發明之方法所製備之鈦-矽分子篩之平均粒徑可超 微米以上’適合用於製備環己酮砖之製程中作為角! 發明亦提供—種製備環己赌之方法,該方法係孩 t月t法所獲彳寸之大粒彳H⑦分子篩作為觸媒,在溶 條件下,以環己酮、氨、及雙氧水進行反應,製 3晴產物。通常,該反應係於1大氣>1或更高之塵 。下、於40 C至110 C之溫度範圍,較佳係於5〇。〇至9〇 度乾圍進行反應。於該反應中,所使用之大粒經分 子師觸媒係占反應物總量之〇.!至⑴ 至5重量%。氨與環⑽之莫耳比錢係丨.2:1至 Π1321 7 201119738 . · 較佳為1.4 : 1至1.8 : 1 ;雙氧水與環己酮之莫耳比範圍係 0.7 : 1至2.0 : 1,較佳為1.0 : 1至1.5 : 1。所使用之雙氧 水濃度可為30%至50%,該雙氧水之進料可隨著反應時間 增加而漸進地加入上述反應系統中。本發明製備環己酮肟 之反應可以在溶劑存在之條件下進行,一般係使用極性溶 劑,例如,醇類、酮類及水等,其中,又以醇類,如第三 丁醇較佳。 以下為本發明方法之多種實施例之例示性說明,並非 用以限制本發明之範圍。 製備例1 先將500毫升圓底燒瓶於真空系統中進行氮封,取 1.98克四正丁基鈦酸酯加入氮封圓底燒瓶,將溫度冷卻至 5°C。接著將20克的無水異丙醇,以注射筒注入上述氮封 圓底燒瓶中,同時開始攪拌。待溫度平衡後,取30克四乙 基矽酸酯,以等壓加料系統逐滴加入氮封圓底燒瓶中,滴 加完成後攪拌1小時。取28克(40%)四正丙基氫氧化銨水 溶液,以等壓加料系統逐滴加入氮封圓底燒瓶中,滴加完 成後攪拌1小時。令系統回溫至室溫後,再攪拌1小時, 最後在80°C下除醇2小時後,加水至總重為100克即可完 成鈦-碎模板劑合成膠。 對照例1 將此製備例1所獲得之鈦-矽模板劑合成膠封入鐵氟 8 111321 * 201119738 . 龍内襯不鏽鋼耐壓罐中,於170°C水熱120小時,將固體 與液體分離後,以純水洗滌固體部份至中性。於100°c乾 燥,500°C煅燒24小時,獲得對照觸媒樣品1,(平均粒徑 為1.1微米,粒徑中位數值(d50)為0.5微采之鈦-矽分子篩)。 實施例1 取0.8克未煅燒鈦-矽分子篩TS-1,以攪拌的方式將 之分散於40毫升水中,加入3.5毫升0.5重量%之陰離子 ®絮凝劑(丙烯酸鈉與丙烯醯銨共聚物,平均分子量為 15.000. 000至20,000,000)水溶液,經攪拌1小時後加入1.5 克四曱基矽酸酯,再攪拌1小時即形成聚集顆粒懸浮液。 將上述聚集顆粒懸浮液與100克製備例1之鈦-矽模 板劑合成膠混合攪拌1小時,然後將此混合液封入鐵氟龍 内襯不鏽鋼耐壓罐中,於170°c水熱120小時,將固體與 液體分離後,以純水洗滌固體部份至中性,於100°c乾燥 鲁及500°C煅燒24小時,即獲得鈦-矽分子篩樣品1。(平均 粒徑為24.2微米,粒徑中位數值(d50)為15.3微米) 實施例2 取用0.7克未煅燒鈦-矽分子篩TS-1,以攪拌的方式 將之分散於40毫升水中,加入1.5毫升0.5重量%之陰 離子絮凝劑(丙烯酸鈉與丙烯醯銨共聚物,平均分子量為 15.000. 000至20,000,000)水溶液,經攪拌1小時後加入0.43 克ES-40,再攪拌1小時即形成聚集顆粒懸浮液。 9 111321 201119738 將上述聚集顆粒懸浮液與100克製備例1之鈦-矽模 板劑合成膠混合攪拌1小時,然後將此混合液封入鐵氟龍 内襯不鏽鋼耐壓罐中,於170°c水熱120小時,將固體與 液體分離後,以純水洗滌固體部份至中性,於l〇〇°C乾燥 及500°C烺燒24小時,即獲得鈦-矽分子篩樣品2。(平均 粒徑為8.9微米,粒徑中位數值(d50)為8.24微米) 實施例3 取用0.7克未煅燒鈦-矽分子篩TS-1,以攪拌的方式 分散於40毫升水中,加入0.2毫升0.5重量%之陰離子 絮凝劑(丙烯酸鈉與丙烯醯銨共聚物,平均分子量為 15,000,000至20,000,000)水溶液,經攪拌1小時後加入0.43 克ES-40,再攪拌1小時即形成聚集顆粒懸浮液。 將上述聚集顆粒懸浮液與100克製備例1之鈦-矽模 板劑合成膠混合攪拌1小時,然後將此混合液封入鐵氟龍 内襯不鏽鋼耐壓罐中,於17〇°C水熱192小時,將固體與 液體分離後,以純水洗滌固體部份至中性,於l〇〇°C乾燥 及500°C煅燒24小時,即獲得鈦-矽分子篩樣品3。(平均 粒徑為14.7微米,粒徑中位數值(d50)為11.9微米) 實施例4 取用0.7克未煅燒鈦-矽分子篩TS-1,以攪拌的方式 分散於40毫升水中,加入1.5毫升0.5重量%之陰離子絮 凝劑(丙稀酸納與丙稀臨敍共聚物,平均分子量為 30 111321 201119738 、 15.000. 000至20,000,000)水溶液,經攪拌1小時後加入The titanium-germanium molecular sieve prepared by the method of the invention may have an average particle diameter of more than micrometers. 'It is suitable for use in the process for preparing cyclohexanone bricks as an angle! The invention also provides a method for preparing a ring gambling method. The large-sized 彳H7 molecular sieve obtained by the method of the t-month is used as a catalyst, and reacted with cyclohexanone, ammonia, and hydrogen peroxide under dissolved conditions to produce a 3 clear product. Usually, the reaction is carried out in a dust of 1 atmosphere > 1 or higher. Lower, in the temperature range of 40 C to 110 C, preferably 5 〇. 〇 〇 to 9 〇 dry circumference to carry out the reaction. In the reaction, the large particles used by the molecular sieves account for (.! to (1) to 5% by weight of the total amount of the reactants. The molar ratio of ammonia to ring (10) is 2:1 to Π1321 7 201119738 . · preferably 1.4 : 1 to 1.8 : 1 ; the molar ratio of hydrogen peroxide to cyclohexanone is 0.7 : 1 to 2.0 : 1 Preferably, it is from 1.0:1 to 1.5:1. The hydrogen peroxide concentration used may be from 30% to 50%, and the hydrogen peroxide feed may be gradually added to the above reaction system as the reaction time increases. The reaction for producing cyclohexanone oxime of the present invention can be carried out in the presence of a solvent, and generally a polar solvent such as an alcohol, a ketone or water is used, and among them, an alcohol such as a butanol is preferred. The following is illustrative of various embodiments of the method of the invention and is not intended to limit the scope of the invention. Preparation Example 1 A 500 ml round bottom flask was first sealed with nitrogen in a vacuum system, and 1.98 g of tetra-n-butyl titanate was placed in a nitrogen-sealed round bottom flask, and the temperature was cooled to 5 °C. Next, 20 g of anhydrous isopropanol was poured into the above nitrogen-sealed round bottom flask in a syringe while stirring was started. After the temperature was equilibrated, 30 g of tetraethyl phthalate was taken and added dropwise to a nitrogen-sealed round bottom flask with an equal pressure feeding system, and the mixture was stirred for 1 hour after the completion of the dropwise addition. A solution of 28 g (40%) of tetra-n-propylammonium hydroxide in water was added dropwise to the nitrogen-sealed round bottom flask in an isostatically charged system, and the mixture was stirred for 1 hour after completion of the dropwise addition. After the system was warmed to room temperature, it was stirred for another hour. Finally, after removing the alcohol for 2 hours at 80 ° C, water was added to a total weight of 100 g to complete the titanium-crushing template synthetic rubber. Comparative Example 1 The titanium-ruthenium template synthetic rubber obtained in Preparation Example 1 was sealed in iron fluoride 8 111321 * 201119738 . The dragon-lined stainless steel pressure tank was heated at 170 ° C for 120 hours to separate the solid from the liquid. The solid portion was washed with pure water to neutrality. After drying at 100 ° C and calcination at 500 ° C for 24 hours, a control catalyst sample 1 (a titanium-germanium molecular sieve having an average particle diameter of 1.1 μm and a median diameter (d50) of 0.5 μM) was obtained. Example 1 0.8 g of uncalcined titanium-rhenium molecular sieve TS-1 was taken and dispersed in 40 ml of water by stirring, and 3.5 ml of 0.5% by weight of an anionic® flocculant (sodium acrylate and acrylonitrile copolymer) was added. An aqueous solution having a molecular weight of 15.000.000 to 20,000,000) was stirred for 1 hour, and then 1.5 g of tetradecyl phthalate was added thereto, followed by stirring for 1 hour to form a suspension of aggregated particles. The above aggregated particle suspension was mixed with 100 g of the titanium-ruthenium template synthetic rubber of Preparation Example 1 and stirred for 1 hour, and then the mixture was sealed in a Teflon-lined stainless steel pressure-resistant tank, and heated at 170 ° C for 120 hours. After separating the solid and the liquid, the solid portion was washed with pure water to neutrality, and dried at 100 ° C for 24 hours at 500 ° C to obtain a titanium-germanium molecular sieve sample 1. (The average particle diameter was 24.2 μm, and the median diameter (d50) was 15.3 μm.) Example 2 0.7 g of uncalcined titanium-rhenium molecular sieve TS-1 was taken and dispersed in 40 ml of water by stirring. 1.5 ml of 0.5% by weight of an anionic flocculant (sodium acrylate and propylene yttrium ammonium copolymer, average molecular weight of 15.000 to 20,000,000) aqueous solution, after stirring for 1 hour, 0.43 g of ES-40 was added, and stirring was further carried out for 1 hour to form aggregated granules. suspension. 9 111321 201119738 The above aggregated particle suspension was mixed with 100 g of the titanium-ruthenium template synthetic rubber of Preparation Example 1 and stirred for 1 hour, and then the mixture was sealed in a Teflon-lined stainless steel pressure-resistant tank at 170 ° C. After heating for 120 hours, the solid was separated from the liquid, and the solid portion was washed with pure water to neutrality, dried at 1 ° C and calcined at 500 ° C for 24 hours to obtain a titanium-ruthenium molecular sieve sample 2. (The average particle diameter was 8.9 μm, and the median diameter (d50) was 8.24 μm.) Example 3 0.7 g of uncalcined titanium-rhenium molecular sieve TS-1 was used, dispersed in 40 ml of water with stirring, and 0.2 ml was added. An aqueous solution of 0.5% by weight of an anionic flocculant (sodium acrylate and propylene yttrium ammonium copolymer having an average molecular weight of 15,000,000 to 20,000,000) was stirred for 1 hour, and then 0.43 g of ES-40 was added, and stirred for 1 hour to form an aggregated particle suspension. The above aggregated particle suspension was mixed with 100 g of the titanium-ruthenium template synthetic rubber of Preparation Example 1 and stirred for 1 hour, and then the mixture was sealed in a Teflon-lined stainless steel pressure-resistant tank at 215 ° C. After the separation of the solid and the liquid, the solid portion was washed with pure water to neutrality, dried at 10 ° C and calcined at 500 ° C for 24 hours to obtain a titanium-germanium molecular sieve sample 3. (The average particle diameter was 14.7 μm, and the median diameter (d50) was 11.9 μm.) Example 4 0.7 g of uncalcined titanium-rhenium molecular sieve TS-1 was used, dispersed in 40 ml of water with stirring, and 1.5 ml was added. 0.5% by weight of anionic flocculant (sodium acrylate and propylene copolymer, average molecular weight of 30 111321 201119738, 15.000.000 to 20,000,000) aqueous solution, added after stirring for 1 hour

I 1.008克ES-40,再攪拌1小時即形成聚集顆粒懸浮液。 將上述聚集顆粒懸浮液與100克製備例1之鈦-矽模 板劑合成膠混合攪拌1小時,然後將此混合液封入鐵氟龍 内襯不鏽鋼耐壓罐中,於170°C水熱120小時,將固體與 液體分離後,以純水洗滌固體部份至中性,於l〇〇°C乾燥 及500°C煅燒24小時,即獲得鈦-矽分子篩樣品4。(平均 粒徑為8.4微米,粒徑中位數值(d50)為7.8微米) 實施例5 取用8.64克未煅燒鈦-矽分子篩TS-1,以攪拌的方式 分散於40毫升水中,加入1.5毫升0.5重量%之陰離子絮 凝劑(丙烯酸納與丙稀驢銨共聚物,平均分子量為 15.000. 000至20,000,000)水溶液,經攪拌1小時後加入0.43 克ES-40,再攪拌1小時即形成聚集顆粒懸浮液。 Φ 將上述聚集顆粒懸浮液與100克製備例1之鈦-矽模 板劑合成膠混合攪拌1小時,然後將此混合液封入鐵氟龍 内襯不鏽鋼耐壓罐中,於160°c水熱240小時,將固體與 液體分離後,以純水洗滌固體部份至中性,於100°c乾燥 及500°c烺燒24小時,即獲得鈦-矽分子篩觸媒樣品5。(平 均粒徑為5.9微米,粒徑中位數值(d50)為5.3微米) 實施例6 取用0.6克未煅燒鈦-矽分子篩TS-1,以攪拌的方式 11 111321 201119738 . 將之分散於40毫升水中,加入0.2毫升0.5重量%之陽 離子絮凝劑(二甲基-二烯丙基氯化銨聚合物,平均分子量 為8,000,000至12,000,000)水溶液,經攪拌1小時後加入 0.43克ES-40,再攪拌1小時即形成聚集顆粒懸浮液。 將上述聚集顆粒懸浮液與100克製備例1之鈦-矽模 板劑合成膠混合攪拌1小時,然後將此混合液封入鐵氟龍 内襯不鏽鋼耐壓罐中,於170°C水熱120小時,將固體與 液體分離後,以純水洗滌固體部份至中性,於l〇〇°C乾燥 及500°C煅燒24小時,即獲得鈦-矽分子篩樣品6。(平均 粒徑為15.3微米,粒徑中位數值(d5〇)為13.1微米) 實施例7 取用0.6克未煅燒矽分子篩S-1,以攪拌的方式將之 分散於40毫升水中,加入0.2毫升0.5重量%之陰離子絮 凝劑(丙烯酸鈉與丙烯醯銨共聚物,平均分子量為 15,000,000至20,000,000)水溶液,經攪拌1小時後加入0.43 克ES-40,再攪拌1小時即形成聚集顆粒懸浮液。 將上述聚集顆粒懸浮液與100克製備例1之鈦-矽模 板劑合成膠混合攪拌1小時,然後將此混合液封入鐵氟龍 内襯不鏽鋼耐壓罐中,於170°C水熱120小時,將固體與 液體分離後,以純水洗滌固體部份至中性,於100°C乾燥 及500°C煅燒24小時,即獲得鈦-矽分子篩樣品7。(平均 粒徑為12.6微米,粒徑中位數值(d50)為9.9微米) 12 111321 201119738 , 實施例8 取用8.64克未煅燒矽分子篩S-l,以攪拌的方式分散 於40毫升水中,加入1.5毫升0.5重量%之陰離子絮凝劑 (丙烯酸鈉與丙烯醯銨共聚物,平均分子量為15,000,000 至20,000,000)水溶液,經攪拌1小時後加入0.43克ES-40, 再攪拌1小時即形成聚集顆粒懸浮液。 將上述聚集顆粒懸浮液與100克製備例1之鈦-矽模 板劑合成膠混合攪拌1小時,然後將此混合液封入鐵氟龍 •内襯不鏽鋼耐壓罐中,於170°c水熱168小時,將固體與 液體分離後,以純水洗滌固體部份至中性,於l〇〇°C乾燥 及500°C煅燒24小時,即獲得鈦-矽分子篩樣品8。(平均 粒徑為10.4微米,粒徑中位數值(d5〇)為8.1微米) 實施例9 取用2.16克未煅燒矽分子篩S-1,以攪拌的方式將之 鲁分散於40毫升水中,加入1.5毫升0.5重量%之陰離子絮 凝劑(丙烯酸鈉與丙烯醯銨共聚物,平均分子量為 15,000,000至20,000,000)水溶液,經攪拌1小時後加入1.06 克AS-40,再攪拌1小時即形成聚集顆粒懸浮液.。 將上述聚集顆粒懸浮液與100克製備例1之鈦-矽模 板劑合成膠混合攪拌1小時,然後將此混合液封入鐵氟龍 内襯不鏽鋼耐壓罐中,於170°C水熱120小時,將固體與 液體分離後,以純水洗滌固體部份至中性,於100°c乾燥 及500°c煅燒24小時,即獲得鈦-矽分子篩樣品9。(平均 13 111321 201119738 粒徑為9.3微米,粒徑中位數值(d50)為6.9微米) 實施例10 取用2.16克未煅燒矽分子篩S-1,以攪拌的方式將之 分散於40毫升水中,加入1.5毫升0.5重量%之陰離子絮 凝劑(丙烯酸鈉與丙烯醯銨共聚物,平均分子量為 15.000. 000至20,000,000)水溶液,經攪拌1小時後加入 0.4244克四甲基矽酸酯,再攪拌1小時即形成聚集顆粒懸 浮液。 將上述聚集顆粒懸浮液與100克製備例1之鈦-矽模 板劑合成膠混合攪拌1小時,然後將此混合液封入鐵氟龍 内襯不鏽鋼耐壓罐中,於170°c水熱120小時,將固體與 液體分離後,以純水洗滌固體部份至中性,於l〇〇°C乾燥 及500°C烺燒24小時,即獲得鈦-矽分子篩樣品10。(平均 粒徑為6.5微米,粒徑中位數值(d50)為5.7微米) 實施例11 取用2.16克未煅燒矽分子篩S-1,以攪拌的方式將之 分散於40毫升水中,加入1.5毫升0.5重量%之陰離子絮 凝劑(丙烯酸鈉與丙烯醯銨共聚物,平均分子量為 15.000. 000至20,000,000)水溶液,經攪拌1小時後加入 0.4180克四乙基矽酸酯,再攪拌1小時即形成聚集顆粒懸 浮液。 將上述聚集顆粒懸浮液與100克製備例1之鈦-矽模 14 111321 201119738 . 板劑合成膠混合攪拌1小時,然後將此混合液封入鐵氤龍I 1.008 g of ES-40 was stirred for an additional hour to form an aggregated particle suspension. The above aggregated particle suspension was mixed with 100 g of the titanium-ruthenium template synthetic rubber of Preparation Example 1 and stirred for 1 hour, and then the mixture was sealed in a Teflon-lined stainless steel pressure-resistant tank, and heated at 170 ° C for 120 hours. After separating the solid and the liquid, the solid portion was washed with pure water to neutrality, dried at 10 ° C and calcined at 500 ° C for 24 hours to obtain a titanium-germanium molecular sieve sample 4. (Average particle diameter was 8.4 μm, and the median diameter (d50) was 7.8 μm.) Example 5 8.64 g of uncalcined titanium-rhenium molecular sieve TS-1 was taken and dispersed in 40 ml of water with stirring, and 1.5 ml was added. 0.5% by weight of an anionic flocculant (copolymer of sodium acrylate and acrylonitrile, average molecular weight of 15.000.000 to 20,000,000) aqueous solution, after stirring for 1 hour, 0.43 g of ES-40 was added, and stirring was further carried out for 1 hour to form agglomerated particles. liquid. Φ The above aggregated particle suspension was mixed with 100 g of the titanium-ruthenium template synthetic rubber of Preparation Example 1 and stirred for 1 hour, and then the mixture was sealed in a Teflon-lined stainless steel pressure-resistant tank at 160 ° C. After the solid was separated from the liquid, the solid portion was washed with pure water to neutrality, dried at 100 ° C and calcined at 500 ° C for 24 hours to obtain a titanium-ruthenium molecular sieve catalyst sample 5. (The average particle diameter was 5.9 μm, and the median diameter (d50) was 5.3 μm.) Example 6 0.6 g of uncalcined titanium-rhenium molecular sieve TS-1 was taken in a stirring manner 11 111321 201119738 . In ml of water, add 0.2 ml of a 0.5% by weight aqueous solution of cationic flocculant (dimethyl-diallylammonium chloride polymer, average molecular weight of 8,000,000 to 12,000,000). After stirring for 1 hour, add 0.43 g of ES-40. The agglomerated particle suspension was formed by stirring for 1 hour. The above aggregated particle suspension was mixed with 100 g of the titanium-ruthenium template synthetic rubber of Preparation Example 1 and stirred for 1 hour, and then the mixture was sealed in a Teflon-lined stainless steel pressure-resistant tank, and heated at 170 ° C for 120 hours. After separating the solid from the liquid, the solid portion was washed with pure water to neutrality, dried at 10 ° C and calcined at 500 ° C for 24 hours to obtain a titanium-germanium molecular sieve sample 6. (The average particle diameter was 15.3 μm, and the median value of the particle diameter (d5〇) was 13.1 μm.) Example 7 0.6 g of uncalcined cerium molecular sieve S-1 was taken, and it was dispersed in 40 ml of water by stirring, and 0.2 was added. An aqueous solution of 0.5% by weight of an anionic flocculant (sodium acrylate and propylene yttrium ammonium copolymer, average molecular weight of 15,000,000 to 20,000,000) was added, and after stirring for 1 hour, 0.43 g of ES-40 was added, and stirring was further carried out for 1 hour to form an aggregated particle suspension. The above aggregated particle suspension was mixed with 100 g of the titanium-ruthenium template synthetic rubber of Preparation Example 1 and stirred for 1 hour, and then the mixture was sealed in a Teflon-lined stainless steel pressure-resistant tank, and heated at 170 ° C for 120 hours. After separating the solid and the liquid, the solid portion was washed with pure water to neutrality, dried at 100 ° C and calcined at 500 ° C for 24 hours to obtain a titanium-germanium molecular sieve sample 7. (average particle diameter was 12.6 μm, median diameter (d50) was 9.9 μm) 12 111321 201119738 , Example 8 8.64 g of uncalcined cerium molecular sieve Sl was taken, dispersed in 40 ml of water with stirring, and 1.5 ml was added. An aqueous solution of 0.5% by weight of an anionic flocculant (sodium acrylate and propylene yttrium ammonium copolymer having an average molecular weight of 15,000,000 to 20,000,000) was stirred for 1 hour, and then 0.43 g of ES-40 was added, and stirred for 1 hour to form an aggregated particle suspension. The above aggregated particle suspension was mixed with 100 g of the titanium-ruthenium template synthetic rubber of Preparation Example 1 and stirred for 1 hour, and then the mixture was sealed in a Teflon® lined stainless steel pressure tank, and heated at 170 ° C. After the solid was separated from the liquid, the solid portion was washed with pure water to neutrality, dried at 10 ° C and calcined at 500 ° C for 24 hours to obtain a titanium-germanium molecular sieve sample 8. (The average particle diameter is 10.4 μm, and the median diameter (d5〇) is 8.1 μm.) Example 9 2.16 g of uncalcined cerium molecular sieve S-1 was taken and dispersed in 40 ml of water by stirring. 1.5 ml of 0.5% by weight of an anionic flocculant (sodium acrylate and propylene yttrium ammonium copolymer, average molecular weight of 15,000,000 to 20,000,000) aqueous solution, after stirring for 1 hour, adding 1.06 g of AS-40, and stirring for 1 hour to form an aggregated particle suspension . . . The above aggregated particle suspension was mixed with 100 g of the titanium-ruthenium template synthetic rubber of Preparation Example 1 and stirred for 1 hour, and then the mixture was sealed in a Teflon-lined stainless steel pressure-resistant tank, and heated at 170 ° C for 120 hours. After separating the solid from the liquid, the solid portion was washed with pure water to neutrality, dried at 100 ° C and calcined at 500 ° C for 24 hours to obtain a titanium-germanium molecular sieve sample 9. (Average 13 111321 201119738 Particle size 9.3 microns, median particle size (d50) is 6.9 microns) Example 10 2.16 grams of uncalcined cerium molecular sieve S-1 was taken and dispersed in 40 ml of water with stirring. Add 1.5 ml of 0.5% by weight of an anionic flocculant (sodium acrylate and propylene yttrium ammonium copolymer, average molecular weight of 15.000.000 to 20,000,000) aqueous solution. After stirring for 1 hour, add 0.4244 g of tetramethyl phthalate and stir for another hour. That is, an aggregated particle suspension is formed. The above aggregated particle suspension was mixed with 100 g of the titanium-ruthenium template synthetic rubber of Preparation Example 1 and stirred for 1 hour, and then the mixture was sealed in a Teflon-lined stainless steel pressure-resistant tank, and heated at 170 ° C for 120 hours. After separating the solid and the liquid, the solid portion was washed with pure water to neutrality, dried at 1 ° C and calcined at 500 ° C for 24 hours to obtain a titanium-germanium molecular sieve sample 10. (The average particle diameter was 6.5 μm, and the median diameter (d50) was 5.7 μm.) Example 11 2.16 g of uncalcined cerium molecular sieve S-1 was taken, and it was dispersed in 40 ml of water by stirring, and 1.5 ml was added. 0.5% by weight of an anionic flocculant (sodium acrylate and propylene yttrium ammonium copolymer, average molecular weight of 15.000 to 20,000,000) aqueous solution, after stirring for 1 hour, 0.4180 g of tetraethyl phthalate was added, and stirring was further carried out for 1 hour to form agglomeration. Particle suspension. The above aggregated particle suspension was mixed with 100 g of the titanium-xyl mold 14 111321 201119738 of the preparation example 1 and the plate synthetic rubber was mixed for 1 hour, and then the mixture was sealed into the iron scorpion dragon.

I 内襯不鏽鋼耐壓罐中,於170°C水熱120小時,將固體與 液體分離後,以純水洗滌固體部份至中性,於l〇〇°C乾燥 及500°C烺燒24小時,即獲得鈦-矽分子篩樣品11。(平均 粒徑為8.2微米,粒徑中位數值(d50)為6.6微米) 實施例12 取用0.6克未煅燒矽分子篩S-1,以攪拌的方式將之 鲁分散於40毫升水中,加入0.2毫升0.5重量%之陽離子絮 凝劑(二曱基-二烯丙基氯化銨聚合物,8,000,000至 12,000,000)水溶液,經攪拌1小時後加入0.43克ES-40, 再攪拌1小時即形成聚集顆粒懸浮液。 將上述聚集顆粒懸浮液與100克製備例1之鈦-矽模 板劑合成膠混合攪拌1小時,然後將此混合液封入鐵氟龍 内襯不鏽鋼耐壓罐中,於170°c水熱120小時,將固體與 籲液體分離後,以純水洗滌固體部份至中性,於100°c乾燥 及500°c烺燒24小時,即獲得鈦-矽分子篩樣品12。(平均 粒徑為8.5微米,粒徑中位數值(d50)為7.5微米之觸媒) 實施例13 取用8.64克未煅燒矽分子篩S-1,以攪拌的方式將之 分散於40毫升水中,加入1.5毫升0.5重量%之陽離子絮 凝劑(二曱基-二烯丙基氯化銨聚合物,8,000,000至 12,000,000)水溶液,經攪拌1小時後加入1.061克AS-40, 15 111321 201119738 再攪拌1小時即形成聚集顆粒懸浮液。 將上述聚集顆粒懸浮液與100克製備例1之鈦-矽模 板劑合成膠混合攪拌1小時,然後將此混合液封入鐵氟龍 内襯不鏽鋼耐壓罐中,於180°c水熱120小時,將固體與 液體分離後,以純水洗滌固體部份至中性,於l〇〇°C乾燥 及500°C煅燒24小時,即獲得鈦-矽分子篩樣品13。(平均 粒徑為9.7微米,粒徑中位數值(d50)為7.6微米) 實施例14 將上述對照例1與實施例1至13所形成之鈦-矽分子 篩樣品作為觸媒,進行環己酮肟之製備以評估其活性。 首先,各取0.55克觸媒樣品置於三頸瓶中,加入5 克環己酮及5.43克之28%氨水,裝上冷凝管及攪拌系統。 將反應溫度升至60°C後,隨反應時間步進式地加入5.43 克之35重量%雙氧水之水溶液,進行環己酮將之製備反 應。雙氧水進料完成後1小時,將各觸媒與其反應液分離, 並對該分離後之各反應液進行環己酮肟之分析。其分析結 果如表1 : 16 111321 201119738 表1 *CAnoe *S〇xime/Anoe ***CH2〇2 ****S〇xiinee2〇2 平均粒徑 (微米) 對照例1 99.75% 98.28% 99.91% 88.75% 1.1 實施例1 99.27% 99.99% 99.26% 91.40% 24.2 實施例2 99.25% 99.57% 99.53% 90.31% 8.9 實施例3 99.63% 99.25% 98.92% 90.87% 14.7 實施例4 99,14% 99,66% 99.99% 89.82% 8.4 實施例5 99.35% 99.52% 99.36% 90.15% 5.9 實施例6 99.67% 99.03% 98.97% 91.50% 15.3 實施例7 99.02% 99.24% 99.97% 89.39% 12.6 實施例8 99.21% 98.49% 99.21% 89.50% 10.4 實施例9 99.53% 98.92% 99.35% 90.48% 9.3 實施例10 98.65% 98.37% 98.79% 90.30% 6.5 實施例11 97.49% 98.89% 97.84% 90.41% 8.2 實施例12 99.40% 98.84% 98.89% 92.20% 8.5 實施例13 99.20% 99.21% 99.52% 89.95% 9.7 *: cAn()e=環己酮轉化率=環己酮消耗莫耳數/環己酮投 入莫耳數χίοο% : s0xime/Alloe=環己酮肟選擇率=環己酮肟產出莫耳數/ 環己酮消耗莫耳數xl00% ***: cH202=雙氧水轉化率=雙氧水消耗莫耳數/雙氧水投 入莫耳數χίοο% : S0xime/H202 =雙氧水選擇率=環己酮肟產出莫耳數/雙 氧水消耗莫耳數χίοο% 17 111321 201119738 t 綜上所述’本發明大粒徑鈇4分 每制 備出利於產業應用之大粒徑分 衣確只衣 肚 ^ 刀子師,且依據本案製法所势 備之大粒控分子篩具有高觸媒、 之大銓钶八工Θ 4 m 依媒本案製法所製備 有产於諸如環己_製程作為觸媒,其具 有衣己i同蔣南選擇率盘名鐘 〆、 更鮝且古h 轉率,以及雙氧水高使用率, 更录具有易於回收之優點。 上述况明書及實施例僅為例示性說明本發明之原理 非用於限制本發明。本發明之權利保護範圍, 應如後述之申請專利範圍所列。 图 【圖式簡單說明】 【主要元件符號說明】 益。 111321 18I Lining stainless steel pressure tank, water heating at 170 ° C for 120 hours, separating the solid and liquid, washing the solid part with pure water to neutral, drying at l ° ° C and 500 ° C simmering 24 The titanium-germanium molecular sieve sample 11 was obtained in an hour. (The average particle diameter was 8.2 μm, and the median diameter (d50) was 6.6 μm.) Example 12 0.6 g of uncalcined cerium molecular sieve S-1 was taken and dispersed in 40 ml of water by stirring, and 0.2 was added. 0.5% by weight of a cationic flocculant (dimercapto-diallylammonium chloride polymer, 8,000,000 to 12,000,000) aqueous solution, after stirring for 1 hour, 0.43 g of ES-40 was added, and stirring was further carried out for 1 hour to form agglomerated particles. liquid. The above aggregated particle suspension was mixed with 100 g of the titanium-ruthenium template synthetic rubber of Preparation Example 1 and stirred for 1 hour, and then the mixture was sealed in a Teflon-lined stainless steel pressure-resistant tank, and heated at 170 ° C for 120 hours. After separating the solid from the liquid, the solid portion was washed with pure water to neutrality, dried at 100 ° C and calcined at 500 ° C for 24 hours to obtain a titanium-germanium molecular sieve sample 12. (Catalyst having an average particle diameter of 8.5 μm and a median diameter (d50) of 7.5 μm) Example 13 8.64 g of uncalcined cerium molecular sieve S-1 was taken and dispersed in 40 ml of water by stirring. Add 1.5 ml of a 0.5% by weight aqueous solution of cationic flocculant (dimercapto-diallylammonium chloride polymer, 8,000,000 to 12,000,000), stir for 1 hour, then add 1.061 g of AS-40, 15 111321 201119738 and stir for another hour. That is, an aggregated particle suspension is formed. The above aggregated particle suspension was mixed with 100 g of the titanium-ruthenium template synthetic rubber of Preparation Example 1 and stirred for 1 hour, and then the mixture was sealed in a Teflon-lined stainless steel pressure-resistant tank, and heated at 180 ° C for 120 hours. After separating the solid and the liquid, the solid portion was washed with pure water to neutrality, dried at 1 ° C and calcined at 500 ° C for 24 hours to obtain a titanium-germanium molecular sieve sample 13. (Average particle diameter was 9.7 μm, and the median value (d50) of the particle diameter was 7.6 μm.) Example 14 A sample of the titanium-germanium molecular sieve formed in the above Comparative Example 1 and Examples 1 to 13 was used as a catalyst to carry out cyclohexanone. Preparation of sputum to assess its activity. First, 0.55 g of the catalyst sample was placed in a three-necked flask, and 5 g of cyclohexanone and 5.43 g of 28% aqueous ammonia were added, and a condenser and a stirring system were installed. After the reaction temperature was raised to 60 ° C, 5.43 g of a 35 wt% aqueous solution of hydrogen peroxide was added stepwise to the reaction time to carry out a reaction of cyclohexanone. One hour after the completion of the hydrogen peroxide feed, each catalyst was separated from the reaction liquid, and each of the separated reaction liquids was subjected to analysis of cyclohexanone oxime. The results of the analysis are shown in Table 1: 16 111321 201119738 Table 1 *CAnoe *S〇xime/Anoe ***CH2〇2 ****S〇xiinee2〇2 Average particle size (micron) Comparative Example 1 99.75% 98.28% 99.91% 88.75% 1.1 Example 1 99.27% 99.99% 99.26% 91.40% 24.2 Example 2 99.25% 99.57% 99.53% 90.31% 8.9 Example 3 99.63% 99.25% 98.92% 90.87% 14.7 Example 4 99, 14% 99, 66% 99.99% 89.82% 8.4 Example 5 99.35% 99.52% 99.36% 90.15% 5.9 Example 6 99.67% 99.03% 98.97% 91.50% 15.3 Example 7 99.02% 99.24% 99.97% 89.39% 12.6 Example 8 99.21% 98.49% 99.21% 89.50% 10.4 Example 9 99.53% 98.92% 99.35% 90.48% 9.3 Example 10 98.65% 98.37% 98.79% 90.30% 6.5 Example 11 97.49% 98.89% 97.84% 90.41% 8.2 Example 12 99.40% 98.84% 98.89% 92.20% 8.5 Example 13 99.20% 99.21% 99.52% 89.95% 9.7 *: cAn()e=cyclohexanone conversion rate=cyclohexanone consumption mole number/cyclohexanone input mole number χίοο% : s0xime/Alloe=cyclohexene Ketone oxime selectivity = cyclohexanone oxime production mole number / cyclohexanone consumption mole number xl00% ***: cH202 = hydrogen peroxide conversion rate = hydrogen peroxide consumption mole number / double oxygen Input Moir χίοο% : S0xime/H202 = Hydrogen peroxide selectivity = cyclohexanone oxime yield Molar number / hydrogen peroxide consumption Molar number χίοο% 17 111321 201119738 t In summary, the invention has a large particle size of 4 points per The large-size granules that are beneficial to industrial applications are indeed only the knives, and the large-sized molecular sieves prepared according to the method of the present invention have a high catalytic activity, and are made up of 8 m according to the preparation method of the medium. It is produced in such a way as a catalyst, which has the advantages of clothing and clothing, the choice of the name of the Jiangnan, the more impressive and the high rate of hydrogen peroxide, and the advantages of easy recycling. The above description and examples are merely illustrative of the principles of the invention and are not intended to limit the invention. The scope of protection of the present invention should be as set forth in the scope of the patent application to be described later. Figure [Simple description of the diagram] [Explanation of main component symbols] Benefits. 111321 18

Claims (1)

201119738 七、申請專利範圍: 一種大粒徑鈦-矽分子篩之製法,包括: 準備第一級結晶顆粒分子篩的分散液; 於上边刀政/夜中加人絮凝劑及助凝劑,使顆粒聚 集’形成聚集顆粒溶液; 混δ該4木顆粒溶液與鈦_矽模板劑合成 進行水熱步驟 2. 如申請專利範圍第1項 貝又衣法,其中,該第一級結晶顆 粒分子篩係選自未炮^ 4 不版現之鈦-矽分子篩粉末、矽分子篩 粉末或其組合。 3. 如申請專利範圍第1項之刹 貝之衣法,其中,該絮凝劑係選自 :種或多種選自陽離子絮凝劑'陰離子絮凝劑及兩性絮 凝劑所組成群組之絮凝劑。 ” (如申請專利範圍第1項之製法,其中,該絮凝劑係選自 -種或多種選自二甲基·二烯丙基氯倾聚合物、賞甲 基丙稀酸三甲銨基乙醋聚合物、聚乙銨、聚乙•咬、 聚丙烯義與丙烯酿銨之共聚物、丙烯酸鋼與丙稀_ 之共聚物’及丙烯酸季銨鹽與丙烯酸鈉之共聚物 群組之絮凝劑。 、凡 5·如申請專利範圍第i項之製法,其_, /、γ 峙劑的平均 刀子量為100000以上。 6.如申請專利範圍第i項之製法,其+, p,. 甲"亥I喊劑用量範 圍為,以100克之該鈦-矽模板劑合成膠計係〇㈨⑴至 0.05 克。 19 Π1321 201119738 r 7.如申請專利範圍第}項之製法,其中,該絮凝劑係以 凝劑水溶液形式添加。 〃 8· ^申請專利範㈣7項之製法,其中,該絮凝劑水溶液 濃度係0.1至1重量〇/〇。 9. 2申請專利範㈣!項之製法,其中,該助凝劑係選自 -種或多種選自矽酸酯、聚乙氧基矽烷以及二氧化矽膠 體溶液所組成群組之助凝劑。 / 如申》月專利fe圍第1項之製法,其中,該助凝劑用量範 圍為’以1GG克之該鈦·梦模板劑合成膠計係〇 !至6 克。 如申請利範圍第^之製法,其中,該第—級結晶顆 粒分子篩與該鈦-矽模板劑合成膠的重量比範圍係介於 1 : 10 至 1 : 800 〇 士申各月專利範圍帛丨項之製法,其巾,該鈦-石夕模板劑 合成膠係由下列步驟形成: 取鈦源置於氮封反應器中; 將〉 谷劑加入該氮封反應器並混合之; 將石夕源等壓滴入該氮封反應器並混合之; 將板劑等壓滴入該氮封反應器並混合之;以及 除去溶劑形成鈦-矽模板劑合成膠。 士申。月專利範圍第12項之製法,其中,該鈦源係四炫 基鈦酸酯。 士申吻專利範圍第]2項之製法,其中,該矽源係四烷 基矽酸酯。 20 111321 201119738 • I5·如申請專利範圍第12項之製法,其中,該溶劑係無水 異丙醇。 该模板劑係四 該鈦源與矽源 該無水異丙醇 16. 如申請專利範圍第12項之製法,其中 丙基氫氡化銨。 17. 如申請專利範圍第Π項之製法,其中 之莫耳比係介於0.005 : 1至〇.〇6 : 1。 18‘如申請專利範圍第15項之製法,其中 與矽之莫耳比係介於1 : 1至4.5 : 1。 該模板劑與石夕 19. 如申請專利範圍第12項之製法,其中 之莫耳比係介於0.1 : 1至0.5 : 1。 20. 如申請專利範㈣!項之製法,其中,該水 度係介於100至22(TC之範圍。 … ^ ^如申請專利範圍第!項之製法,其t,該水熱步驟之時 間係介於72至240小時之範圍。 22=申請專利範圍第!項之製法,復包括於水熱步驟㈣ 行水洗、烘乾及煅燒步驟。 玖:,利範圍第w之製法,其令,所形成之大粒徑 矽为子篩之平均粒徑係大於5微米。 24.圍Γι造『己:將之方法,該方法係利用如申請專利範 媒’在容齡在之條件下,麵⑽ :隹觸 反應形成環己酮肟。 铽又虱水進仃 以·如申請專利範圍第24項之方法 之莫耳比為1.2 : 1至2 : !。 一、亥風料己酮 ]11321 21 201119738 26. 如申請專利範圍帛%項之方法其中 己酉同之莫耳比為0.7 : 1至2.0 : 1。 27. 如申請專利範圍第24項之方法,其中 溶劑。 該雙氧水與環 該溶劑係極性 28. 如申請專利範圍第27項之方法,其中 選自醇、酮及水所構成之組群。 29. 如申請專利範圍第24項之方法,其中 丁醇。 該極性溶劑係 該溶劑係第三 30.如申請專利範圍第 量’以反應物總重 24項之方法,其中,該觸媒之使用 計係占0.1至10重量% 。 ]]]32J 22 201119738 四、指定代表圖: (一) 本案指定代表圖為:無。 (二) 本代表圖之元件符號簡單說明:無。 本案無圖式。 五、本案若有化學式時,請揭示最能顯示發明特徵的化學式: 。201119738 VII. Patent application scope: A method for preparing a large-diameter titanium-bismuth molecular sieve, comprising: preparing a dispersion of a first-stage crystalline particle molecular sieve; adding a flocculant and a coagulant to the upper knife/night to make the particles aggregate Forming agglomerated particle solution; mixing δ the 4 wood particle solution and titanium 矽 矽 template to synthesize hydrothermal step 2. According to claim 1 of the patent item, the first stage crystal granule molecular sieve is selected from the Guns 4 are not available in titanium-germanium molecular sieve powder, cerium molecular sieve powder or a combination thereof. 3. The method according to claim 1, wherein the flocculating agent is selected from the group consisting of: a flocculant selected from the group consisting of a cationic flocculant 'anionic flocculant and an amphoteric flocculant. (The method of claim 1, wherein the flocculating agent is selected from the group consisting of: one or more selected from the group consisting of dimethyl diallyl chloride deuterated polymer, and methyl methacrylate trimethylammonium ethyl vinegar A flocculant of a copolymer of a polymer, a polyethylammonium, a polyethylene, a bite, a copolymer of polypropylene and propylene, a copolymer of acrylic steel and propylene, and a copolymer of quaternary ammonium acrylate and sodium acrylate. 5. If the method of applying the patent range i is the method of the patent, the average knife amount of the _, /, γ bismuth agent is 100000 or more. 6. If the method of applying the patent range i, the +, p,. A &quot ; Hai I caller dosage range is 100 grams of the titanium-ruthenium template synthetic gel system 〇 (9) (1) to 0.05 grams. 19 Π 1321 201119738 r 7. The method of claim 5, wherein the flocculant system It is added in the form of an aqueous solution of a coagulant. 〃 8· ^ The method of applying the patent formula (4), wherein the concentration of the flocculant aqueous solution is 0.1 to 1 weight 〇 / 〇. 9. 2 Patent Application (4), the method of the item, wherein The coagulant is selected from the group consisting of one or more selected from the group consisting of phthalate esters and polyethoxylates. A coagulant consisting of a mixture of decane and cerium oxide colloidal solution. / The method of the first method of the patent of the patent, wherein the amount of the coagulant is in the range of 1 gram of the titanium-dream template synthesis According to the method of applying the range of the method, wherein the weight ratio of the first-order crystalline particle molecular sieve to the titanium-ruthenium template synthetic rubber is between 1:10 and 1:800. The method for preparing the patent scope of each month, the towel, the titanium-stone templating agent synthetic gel is formed by the following steps: taking a titanium source in a nitrogen sealed reactor; adding a gluten to the nitrogen seal The reactor is mixed and mixed; the isothermal solution is dropped into the nitrogen sealing reactor and mixed; the plate is dropped into the nitrogen sealing reactor and mixed; and the solvent is removed to form a titanium-ruthenium template synthetic rubber. Shishen. The method of the 12th patent range of the patent, wherein the titanium source is a tetrasyl titanate. The method of the patent scope is the second method, wherein the source is a tetraalkyl phthalate. 20 111321 201119738 • I5·If the method of applying for the scope of patent 12 is Wherein, the solvent is anhydrous isopropanol. The template is the titanium source and the source of the anhydrous isopropanol. 16. The method of claim 12, wherein the propyl hydroquinone ammonium. The method of the third paragraph of the patent scope, wherein the molar ratio is between 0.005:1 and 〇.〇6:1. 18', as in the method of claim 15, wherein the molar ratio is between 1 and 1 : 1 to 4.5 : 1. The templating agent and Shi Xi 19. The method of claim 12, wherein the molar ratio is between 0.1:1 and 0.5:1. 20. For example, apply for a patent (4)! The method of the invention, wherein the water system is between 100 and 22 (the range of the TC. ... ^ ^, as in the method of applying the patent scope!, t, the time of the hydrothermal step is between 72 and 240 hours Scope 22: The method of applying for the scope of the patent item is included in the hydrothermal step (4). The steps of washing, drying and calcining are carried out. 玖: The method of the range of w is the method of making the large particle size The average particle size of the sub-screen is greater than 5 microns. 24. The cofferdam is made by "make the method: the method is based on the application of the patent media" under the condition of the age, the surface (10): the reaction reacts to form a ring Ketone oxime. 铽 虱 仃 · · · 如 如 如 如 如 如 如 如 如 如 如 如 如 如 如 如 如 如 如 如 1.2 1.2 1.2 1.2 1.2 1.2 1.2 1.2 1.2 1.2 1.2 1.2 1.2 1.2 1.2 1.2 1.2 1.2 1.2 1.2 1.2 1.2 1.2 1.2 1.2 The method of 5% is the same as the molar ratio of 0.7:1 to 2.0: 1. 27. The method of claim 24, wherein the solvent is used. The hydrogen peroxide and the ring are polar. The method of item 27, wherein the method comprises a group consisting of an alcohol, a ketone and water. The method of claim 24, wherein the butanol is the solvent. The solvent is the third. 30. The method according to the patent application, the quantity 'total weight of the reactants, 24, wherein the catalyst is used. Accounted for 0.1 to 10% by weight.]]]32J 22 201119738 IV. Designation of representative drawings: (1) The representative figure of the case is: No. (2) The symbol of the symbol of the representative figure is simple: No. There is no picture in this case. If there is a chemical formula in this case, please reveal the chemical formula that best shows the characteristics of the invention: 111321111321
TW098142427A 2009-12-11 2009-12-11 Method for preparing large-diameter titanium-silicon molecular sieve and method for producing cyclohexanone oxime using the molecular sieve TWI399242B (en)

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TW098142427A TWI399242B (en) 2009-12-11 2009-12-11 Method for preparing large-diameter titanium-silicon molecular sieve and method for producing cyclohexanone oxime using the molecular sieve
US12/748,932 US8540956B2 (en) 2009-12-11 2010-03-29 Method for preparing titanium-silicalite molecular sieve and method for preparing cyclohexanone oxime using titanium-silicalite molecular sieve
JP2010274894A JP5437984B2 (en) 2009-12-11 2010-12-09 Method for producing large particle size titanium-silicon molecular sieve and method for producing cyclohexanone oxime using the same

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
TWI508935B (en) * 2011-08-11 2015-11-21 China Petrochemical Dev Corp Taipei Taiwan Titanium-silicon molecular sieve and its preparation method and method for producing cyclohexanone oxime using the molecular sieve

Families Citing this family (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US10196275B2 (en) * 2012-10-05 2019-02-05 Basf Se Process for the production of a zeolitic material employing elemental precursors
RU2523547C1 (en) * 2013-05-15 2014-07-20 Федеральное государственное бюджетное образовательное учреждение высшего профессионального образования "Нижегородский государственный технический университет им. Р.Е. Алексеева" НГТУ Method of titanium silicalite encapsulation in polymeric matrix
CN104340988B (en) * 2013-07-31 2016-03-16 中国石油化工股份有限公司 The forming method of HTS and the shaping HTS obtained by the method and application
CN106904632B (en) * 2015-12-23 2019-09-24 中国石油化工股份有限公司 A kind of HTS and its synthetic method and application and a kind of method for hydroxylation of phenol
CN107986294B (en) * 2016-10-27 2020-02-28 中国石油化工股份有限公司 A kind of vanadium-containing titanium-silicon molecular sieve and its synthesis method and application
CN110294484B (en) * 2019-07-29 2022-06-24 青岛科技大学 Nano titanium silicon TS-1 molecular sieve and its synthesis method
JP7556686B2 (en) * 2019-12-26 2024-09-26 日揮触媒化成株式会社 Method for producing titanosilicate zeolite without using raw materials containing alkoxy groups
CN114426500B (en) * 2020-09-21 2024-02-13 中国石油化工股份有限公司 Method for preparing ketoxime by ketoxime
CN112520753B (en) * 2020-10-19 2022-09-23 郑州大学 Method for improving mechanical strength of titanium silicalite TS-1
CN114904572B (en) * 2021-02-08 2024-01-30 中国石油化工股份有限公司 Titanium-silicon molecular sieve catalyst and preparation method and application thereof

Family Cites Families (19)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
IT1127311B (en) * 1979-12-21 1986-05-21 Anic Spa SYNTHETIC, CRYSTALLINE, POROUS MATERIAL CONSTITUTED BY SILICON AND TITANIUM OXIDES, METHOD FOR ITS PREPARATION AND ITS USES
JPS6172621A (en) * 1984-09-14 1986-04-14 Toa Nenryo Kogyo Kk Molded article of binderless zeolite and its production
JPS6172620A (en) * 1984-09-14 1986-04-14 Toa Nenryo Kogyo Kk Molded article of binderless zeolite and its production
IT1213504B (en) * 1986-10-22 1989-12-20 Eniricerche Spa ZEOLITI LEGATE AND PROCEDIMENYE FOR THEIR PROSUCTION.
JP3303341B2 (en) * 1992-07-30 2002-07-22 三菱化学株式会社 Method for producing beta zeolite
PT791558E (en) * 1996-02-22 2002-05-31 Enichem Spa SILICON / ZEOLITE COMPOSITE MATERIALS IN SPHERICAL FORM AND PROCESSES FOR THEIR PREPARATION.
DE19731627A1 (en) * 1997-07-23 1999-01-28 Degussa Granules containing titanium silicalite-l
IT1295267B1 (en) * 1997-10-03 1999-05-04 Enichem Spa PROCESS FOR PREPARING ALLOYED ZEOLITES
DE19939416A1 (en) * 1999-08-20 2001-02-22 Basf Ag Production of zeolite, e.g. titanium zeolite, useful as catalyst (support), sorbent, pigment or filler for plastics, involves crystallizing solid from precursor(s) and direct drying of reaction mixture
ES2178910B1 (en) * 1999-11-24 2003-12-16 Univ Valencia Politecnica HIGH SURFACE MICROPOROUS MATERIALS ACTIVE IN OXIDATION REACTIONS. TIQ-6 AND METIQ-6.
CN1132699C (en) * 1999-12-24 2003-12-31 中国石油化工集团公司 Titanium-silicon molecular sieve and its preparing method
EP1125891A1 (en) * 2000-02-17 2001-08-22 SOLVAY (Société Anonyme) Process for the preparation of a crystalline solid
US6746660B1 (en) * 2002-12-11 2004-06-08 National Central University Process for the production of ultra-fine zeolite crystals and their aggregates
FR2867200B1 (en) * 2004-03-05 2006-05-26 Inst Francais Du Petrole UVL-1 CRYSTALLIZED SOLID AND METHOD FOR HYDROCONVERSION / HYDROCRACKING OF HYDROCARBON LOADS
US20080253959A1 (en) * 2007-03-30 2008-10-16 Johnson Ivy D Synthesis crystalline molecular sieves
ITMI20072342A1 (en) * 2007-12-14 2009-06-15 Polimeri Europa Spa PROCESS TO PREPARE ZEOLITIS TS-1
CN101480622B (en) * 2009-02-13 2010-08-25 中国天辰工程有限公司 A kind of preparation method of large particle size titanium silicon molecular sieve catalyst
CN101486667B (en) * 2009-02-13 2012-06-20 中国天辰工程有限公司 Method for preparing cyclohexanone oxime by fluid bed reactor
CN101596463B (en) * 2009-07-09 2011-01-05 天津大学 Granular titanium-silicon molecular sieve catalyst and preparation method thereof

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
TWI508935B (en) * 2011-08-11 2015-11-21 China Petrochemical Dev Corp Taipei Taiwan Titanium-silicon molecular sieve and its preparation method and method for producing cyclohexanone oxime using the molecular sieve

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